[0001] This invention concerns a melt-processible blend. It also concerns a process for
producing the melt-processible blend and use of the melt-processible blend.
[0002] Polymer blends are very important to the plastics industry and are well known. Miscible
polymer blends, often referred to as polymer alloys, are desirable and useful because
they provide a unique combination of properties from two or more polymers which one
polymer alone cannot provide. In particular, blend polymers such as polymethyl methacrylate
(pMMA) and polycarbonate, for example, bisphenol-A polycarbonate (PC) would be highly
desirable and commercially useful materials for producing miscible transparent polymer
blends. These materials are desirable and useful because pMMA is a clear, relatively
inexpensive polymer with excellent light transmission and resistance to sunlight and
PC is a clear polymer with the advantageous properties of toughness and high heat
resistance. Unfortunately, pMMA lacks heat resistance and is brittle so it cannot
be used in all applications, and PC is a relatively expensive polymer. It is therefore
desirable to achieve fully miscible polymer blends of pMMA and PC. Such blends would
offer variable property/cost behavior properties based on blend ratios of pMMA and
PC between the limits of pure pMMA and pure PC, while maintaining optical clarity.
[0003] Unfortunately, pMMA and PC are known not to be compatible or miscible. Melt processed
blends of pMMA and PC having commercially useful molecular weights, such as weight
average molecular weights of about 70,000 or more, are not homogeneous. Phase separation
of such blends occurs at temperatures just above the glass transition temperature
of the blend. The melt processing temperature required for polycarbonate or PC is
typically 100 degrees Celsius (°C) above its glass transition temperature (Tg), and
in this case about 100°C above the Tg range for polycarbonates, of 150°C to 250°C,
and at that processing temperature, blends of pMMA and PC are inhomogeneous and opaque,
and have undesirable mechanical properties. It is therefore desirable to achieve a
blend of pMMA and PC that remains as a single phase at melt-processing temperatures.
[0004] The "cloud point temperature" is an important factor in blend miscibility, as it
is the temperature at which the blend changes from clear to "cloudy," because of phase
separation. To be melt-processible, the cloud point of the PC and MMA copolymer blend
should be ≧ 250°C. If a comonomer is not particularly efficient at altering the phase
behavior of the blend, a large amount of the comonomer must be added, thus raising
the expense of the copolymer and/or changing the physical properties of methyl methacrylate
polymer.
[0005] US-A- 4,491,647 ('647) discloses a partially miscible blend or a polyblend of polycarbonate
and N-phenylmaleimide-methyl methacrylate copolymer. These partially miscible blends
are taught as ternary compatibilizers for polycarbonates with acrylonitrile-butadiene-styrene
(ABS) resins or rubber-modified styrene-maleic anhydride resins.
[0006] Additional references teach comonomers polymerized with methyl methacrylate to improve
the thermal stability, but which hinder miscibility with PC. For instance, US-A- 5,073,615
and JP 61-162,509 both teach the copolymerization of methyl methacrylate with various
N-substituted maleimide compounds, including methyl, ethyl, phenyl and cyclohexyl
maleimide. Many of these maleimides, however, render the methacrylate copolymer incompatible
with PC resin, particularly phenyl maleimide (PMI), as discussed earlier in '647.
While cyclohexyl maleimide enhances the miscibility with PC, it is not an efficient
comonomer in altering the phase behavior, and as such does not raise the cloud point
sufficiently that all blend ratios are melt-processible. US-A-4,950,716 demonstrates
the copolymerization of cyclohexyl maleimide with methyl methacrylate, but shows that
the cloud points of the blends were not sufficiently raised such that some blend compositions
were opaque after melt-processing.
[0007] EP 483,717 teaches copolymerization of methyl methacrylate with ring-halogenated
phenyl methacrylate, for example tribromophenyl methacrylate. While the tribromophenyl
methacrylate comonomer appears to be somewhat efficient at raising the cloud point
temperature of the blend, relatively large amounts of the comonomer need to be incorporated
into the copolymer, for instance ≧ 20 weight percent (wt%). Further, tribromophenyl
methacrylate has the ability to homopolymerize, and its incorporation into a copolymer
with methyl methacrylate is not straightforward. Special synthetic techniques are
required to prevent homopolymerization of the comonomer, which would result in formation
of an opaque copolymer.
[0008] Therefore, there are deficiencies with the approaches used to achieve fully miscible
blends of pMMA and PC which can be melt-processed. Deficiencies include the molecular
weights of the polymers must be reduced, or the comonomer added to methyl methacrylate
is not efficient or is difficult to polymerize or adds great expense, or comonomer,
such as methacrylate based esters, undesirably changes the properties of the copolymer
especially with regard to thermal stability. In the case where termonomers are needed
to enhance thermal stability, often miscibility with PC is diminished or expense is
added for the manufacture of the copolymer.
[0009] Phase behavior and achieving single phase blends is a function of many factors, particularly
polymer molecular weight (MW) and the polymer-polymer interactions involved. For PC
and pMMA systems, the polymer-polymer interactions are very weak, such that the phase
behavior of the blend is very sensitive to the molecular weight and molecular composition
of the polymers. It is not very advantageous to reduce the molecular weights of the
polymers to achieve a homogeneous blend at melt-processing temperatures, since the
mechanical properties of the polymers also decrease.
[0010] The aim of the invention is to provide a polymer blend with excellent transparency
and thermal resistance.
[0011] In accordance with the present invention there is provided a melt-processible blend
comprising a methyl methacrylate-tribromophenyl maleimide copolymer and polycarbonate,
the weight percent ratio of the copolymer to the polycarbonate being 1:99 to 99:1.
[0012] Applicants have found that methyl methacrylate-tribromophenyl maleimide copolymers
exhibit enhanced miscibility with polycarbonate, such that melt-processible blends
of polycarbonate having excellent transparency and thermal resistance over the entire
range of blend compositions (from 99% of methacrylate copolymer to 99% of polycarbonate)
are possible.
[0013] Applicants found that tribromophenyl maleimide does not homopolymerize, thus it is
possible to form a transparent (sans tribromophenyl maleimide homopolymer) and thermally
stable methyl methacrylate-tribromophenyl maleimide copolymer by conventional polymerization
procedures. Usage of tribromophenyl maleimide comonomer in the copolymer may range
from 10-80 weight percent, preferably from 10-50 weight percent, and most preferably
from 10 to 20 weight percent tribromophenyl maleimide in the copolymer. Since only
a small amount of the comonomer needs to be incorporated into the copolymer, manufacture
of the copolymer does not involve great expense. A melt-processible polymer blend
with excellent transparency and thermal resistance is possible, having a commercially
useful molecular weight of 50-500,000 and preferably 100-200,000 weight average molecular
weight, and satisfying a broad range of properties by alloying polycarbonate and a
methacrylate copolymer containing tribromophenyl maleimide.
[0014] In accordance with the present invention there is also provided a process for producing
the melt-processible blend, comprising the steps of:
(a) preparing a copolymer of methyl methacrylate and tribromophenyl maleimide; and
(b) blending the methyl methacrylate-tribromophenyl maleimide copolymer and polycarbonate.
[0015] Finally, the present invention provides use of the melt-processible blend in a transparent
film, article or moulded material, and preferably in a sky-light, a window, a door,
a laser read compact recording disk, a sign, an athletic playing field enclosure,
and vehicle glazing.
A. Copolymer Synthesis:
[0016] The copolymer of the present invention is composed of methyl methacrylate and tribromophenyl
maleimide, designated herein as "MMA/TBPMI". The copolymerization can be conducted
by any of the typical methods, for instance bulk, solution or emulsion polymerization.
The copolymer exemplified in the examples was made by free radical emulsion copolymerization.
Applicants prepared various compositions of the copolymer, and of particular interest
are compositions 100/0, 90/10, 85/15, 80/20, and 70/30 MMA/TBPMI, where the amounts
shown are weights ratios of the MMA/TBPMI monomers. Initiators, chain transfer agents
and soaps (in the case of emulsion polymerization) can be used, according to widely
known and practiced polymerization techniques. By varying the amounts of initiator,
chain transfer agent and soap, the degree of polymerization, molecular weight, and
the particle size, respectively, can be controlled. For specific procedures used to
prepare the copolymers, see section A.1 Synthesis Examples.
B. Copolymer Blends with PC:
[0017] By blending the methyl methacrylate-tribromophenyl maleimide copolymer with polycarbonate,
it is possible to raise the cloud point temperature such that the blend remains as
a single phase at melt-processing temperatures. In order to demonstrate the usefulness
of the present invention, a description of the phase behavior as a function of temperature
and blend composition is necessary. As shown herein, MMA/TBPMI copolymers form single
phase blends with PC, at all blend ratios, at the temperature required for melt processing.
[0018] Polycarbonates useful herein generally have a Tg ranging from about 100°C to about
300°C, and these polycarbonates include bisphenol A polycarbonate, as exemplified
herein, and which is also known as poly(oxycarbonyloxy-1,4-phenyleneisopropylidene-1,4-phenylene).
[0019] The polycarbonates to be used in this invention are any known in the art, but the
ones based on bisphenol A reacted with carbonyl chloride in an interfacial process
to produce bisphenol-A polycarbonate (PC) are preferred due to their commercial importance
and availability.
[0020] A fully miscible polymer blend, that is, a blend that consists of one phase at the
temperature of interest, evidences itself as a clear material with a single glass
transition temperature (Tg). A number of methods can be used to demonstrate that a
blend is miscible. The most typical method is one in which the polymers are blended
in a given blend ratio and dissolved in a solvent. The solvent solution is cast into
a film, and the film examined for clarity or the presence of a single Tg. If the blend
is not fully miscible, the film will be opaque at room temperature, or become opaque
as the film is heated. The film will also exhibit more than a single glass transition
temperature.
[0021] Unfortunately, erroneous conclusions about the miscibility of a blend can be made,
because phase behavior depends critically on the method of preparation. It is possible
with the solvent-preparation procedure to trap a non-equilibrium yet homogeneous state,
such that the blend appears to be miscible. In particular, poor estimates of the extent
of miscibility between PC and pMMA have been reported in the literature. The most
reliable method for sample preparation is melt-blending, using mixing equipment such
as a Haake Rheocord, manufactured by Haake Company, or a Brabender Plasticord, manufactured
by C.W. Brabender Company. The phase behavior of melt-blended samples is free from
the interfering effects of a solvent. Demonstrating the temperature dependence of
blend phase behavior, however, is difficult by melt-blending, because of changes in
the melt viscosity. Typically, samples of PC are melt-blended only at one temperature,
the "optimal" melt-processing temperature, which is about 250°C.
[0022] The blend may be formed by conventional mixing of polymeric resins, powders or pellets,
such as by tumbling and drum mixing, or may be compounded by means such as roll mills.
Preferred is a single- or twin-screw extruder, which may also be used to form pellets
of the melt-compounded blend for further processing, or may directly conduct the melt
to a separate zone or zones suitable for injection molding or extrusion into sheet
material for blow molding. The extruder may be equipped with a devolatilizing vent.
[0023] The temperature dependence of blend phase behavior can be approximated by methods
known as "cloud point determination" methods. Cloud point temperatures are typically
estimated by heating solution-cast film samples of a hot-stage microscope. Since blends
such as PC/pMMA exhibit slow phase separation, the hot-stage microscope method often
results in an "overestimate" of the cloud point. And as noted above, the observed
cloud point behavior is not necessarily indicative of the thermodynamic phase behavior.
[0024] Applicants therefore developed a differential scanning calorimetry (DSC) experiment
as exemplified, to estimate cloud points and to demonstrate how incorporation of tribromophenyl
maleimide increases the cloud point of the PC/copolymer blend. Samples of "precipitated
polymer" blends were prepared, as described below. Applicants bracketed apparent cloud
points for blend compositions ranging from 100% copolymer through 100% PC. The copolymers
examined were of MMA/TBPMI composition (wt%) 90/10 (example 1b), 80/20 (example 1d)
and 70/30 (example 1e). Applicants also examined a "control" pMMA polymer (Plexiglas®
V811 acrylic resin), a "control" polycarbonate polymer (Makrolon® 2808 polycarbonate),
and a "control" copolymer, MMA/PMI (example 1f).
[0025] Generally, the blends taught herein are useful as transparent materials, films, plates,
shaped articles, molded items for optical purposes such as lenses, prisms, optical
wave guides, optical disk substrates, and construction materials, where durable, tough,
weatherable, and clear features are desired.
[0026] Applications for these blends with excellent transparency, thermal resistance and
toughness include markets such as automotive, sheet (glazing), retail displays, signs,
electronics, business machines, lighting, industrial guards, restaurant fixtures,
art/document preservation and appliances, as well as a number of specialty niches
such as compact disks, ophthalmic lenses, medical, riot-control equipment, transparent
mixing tanks, aircraft canopies and sports equipment such as helmet masks and athletic
playing field enclosures or fencing.
[0027] Automotive applications include tail and side marker lights, headlamps, and supports.
Polycarbonate blends are being used in instrument panels as well as bumpers. An extremely
high potential for polycarbonate blends exists with exterior body parts such as body
panels and wheel covers. Other uses include traffic light housings, signal lenses,
trim and vehicle glazing (windows).
[0028] Clarity, toughness, and high-heat properties make polycarbonate ideal for glazing
applications. With the appropriate UV stabilizer, polycarbonate can replace glass
and impact modified acrylic sheet for use in signs, displays and vandal-proof glazing
applications, such as windows and doors in schools, buildings or homes, or for outdoor
lighting. Ophthalmic lenses and safety glasses are important applications. Hard coatings
are available to increase durability of lenses and glasses.
[0029] Electronics and business machines are also a major market segment. Applications include
connectors, breaker boxes, gears, computer housings, copier housings, and tape housings.
A new application is in laser-read compact recording disks that provide superior high-density
recording quality as well as durability.
[0030] Appliances consume polycarbonate in sizable volumes. High impact, heat, and durability
provide design flexibility for vacuum sweepers, kitchen appliances such as mixing
bowls, refrigerator doors and power tools.
[0031] Food-contact applications include water bottles for water dispensers, microwave ovenware,
beer mugs and pitchers, tableware, restaurant trays and food storage containers. These
products can be designed to be attractive, clear and virtually unbreakable.
[0032] Medical applications also provide high potential growth based on clarity and relative
break-resistance. Sterilization of containers and packages by steam, ethylene oxide,
and gamma radiation are often required. Polycarbonate performs well in this area since
the introduction of grades that can be sterilized with gamma radiation without objectionable
color change.
[0033] Building and construction applications are a relatively untapped market segment where
polycarbonate or its blends could be used if cost-competitive with traditional building
materials. Applications include sky-lights, architectural glazing, windows, kitchen
cabinets and sliding glass doors.
[0034] Concerns about weathering, chemical resistance and scratch resistance can be minimized
by the use of additives, plastic or polymer coatings, or coextrusion technology.
[0035] The individual components of the blend may contain additives normally found in such
materials when purchased commercially. For example, the polycarbonate and methyl methacrylate
may contain one or more impact modifier, thermal stabilizer, ultraviolet stabilizer,
antioxidant or the like.
[0036] Polycarbonate, methyl methacrylate-tribromophenyl maleimide copolymer, and blend
performance and versatility may be enhanced by the use of various additives such as
thermal stabilizers, ultraviolet stabilizer, mold release agents, glass fibers, ignition-resistant
additives, processing aids, antioxidants, impact modifiers, colorants, color concentrates,
flame retardants, lubricants, pigments, and fillers.
[0037] Having described the materials and methods of this invention, the following examples
are presented to illustrate the invention, but not to limit it.
EXAMPLES
[0038] In the following examples, all parts and percentages are by weight unless otherwise
indicated.
A.1 Synthesis Examples:
[0039] The following specific examples exemplify preparation of copolymers tested in blends
with PC:
1(a) 34 parts water and 0.01 parts sodium carbonate were added to a 3 liter reaction
flask. The contents of the flask were purged with a stream of nitrogen gas and heated
to 80°C. A separate monomer mixture was prepared, containing 44 parts of methyl methacrylate,
0.9 parts of n-dodecyl mercaptan, 1 part sodium dodecyl benzene sulfonate, 0.4 parts
sodium bistridecyl sulfosuccinate, 0.01 parts sodium carbonate and 13 parts water.
9% of this separate monomer mixture was added to the reaction flask, along with 0.006
parts sodium persulfate and 1 part water. After five minutes 20% of a solution composed
of 0.02 parts sodium persulfate solution and 6 parts water was added. The remainder
of the separate monomer mixture and the sodium persulfate solution were added dropwise
over 3 hours. The contents of the reaction flask were held at 80°C for an additional
hour, and then cooled and filtered. The copolymerization reaction went to high (>95%)
conversion. Powder was obtained by spray-drying the reaction product.
1(b) A copolymer was prepared by method 1(a), except that 39.6 parts of methyl methacrylate
and 4.4 parts of tribromophenyl maleimide were used.
1(c) A copolymer was prepared by method 1(a), except that 37.4 parts of methyl methacrylate
and 6.6 parts of tribromophenyl maleimide were used.
1(d) A copolymer was prepared by method 1(a), except that 35.2 parts of methyl methacrylate
and 8.8 parts of tribromophenyl maleimide were used.
1(e) A copolymer was prepared by method 1(a), except that 30.8 parts of methyl methacrylate
and 13.2 parts of tribromophenyl maleimide were used.
1(f) A copolymer was prepared by method 1(a), except that 39.6 parts of methyl methacrylate
and 4.4 parts of phenyl maleimide were used.
[0040] A summary of the physical properties of copolymer 1(a)-1(f) appears in Table I. Included
in Table I are properties of the other resins used in the polymer blend experiments,
namely polymethyl methacrylate (Plexiglas® V-811 acrylic resin, a product of Rohm
and Haas Company) and bisphenol-A polycarbonate (Makrolon® 2808 polycarbonate, a product
of Miles Company). The copolymer compositions of examples 1(a)-(f) were verified by
elemental analysis, specifically, percent (%) bromine analysis. The molecular weights
are weight averages obtained from gel-permeation chromotography (GPC) measurements
relative to a polymethyl methacrylate standard. Glass transition temperatures were
measured by DSC, in air, at a scanning rate of 20°C/min. Five percent (5%) weight
loss temperatures were measured by thermal gravimetric analysis (TGA), in air, at
a scanning rate of 20°C/min. Examples 1(d) and 1(f) contain equimolar amounts of phenyl
maleimide moiety, either with bromine atoms (example 1(d)) or without bromine (example
1(f)). In comparing copolymers containing equimolar amounts of tribromophenyl maleimide
(TBPMI) and phenyl maleimide (PMI), TBPMI demonstrates advantages of higher Tg and
better compatibility than PMI in methyl methacrylate. Comparisons between copolymers
1(a)-1(f), described in section B, demonstrate the efficiency with which tribromophenyl
maleimide enhances miscibility with PC (examples 1(b) - 1(e)).
[0041] Tribromophenyl maleimide is commercially available as Actimer FR 1033, a product
of the Dead Sea Bromine Group. Actimer FR 1033 is the 2,4,6-tribromophenyl maleimide
isomer of tribromophenyl maleimide.
2(a) Dilute solutions (5 wt%) were made in tetrahydrofuran (THF) solvent. Blend of
this example consisted of pMMA (Plexiglas® V-811 acrylic resin) and PC (Makrolon®
2808 polycarbonate). Six solutions were prepared, consisting of 20 grams of THF and
1 gram total polymer in these weight ratios: 1) 100 wt% pMMA, 2) 80 wt% pMMA and 20
wt% PC, 3) 60 wt% pMMA and 40 wt% PC, 4) 40 wt% pMMA and 60 wt% PC, 5) 20 wt% pMMA
and 80 wt% PC, and 6) 100 wt% PC. "Precipitated polymer" blend samples were made by
adding each solution to a twenty-fold excess of methanol (the "nonsolvent"). The precipitated
polymer blend was collected on a buchner funnel, dried for 1 hr. in a 70°C oven with
a steady stream of air, and further dried in a vacuum oven for 5 days at 150°C. This
precipitation method eliminates some of the effects of solvent interactions and is
therefore the preferred method of blend sample preparation.
2(b) Precipitated polymer blend samples were made as in 2(a), except that in place
of the Plexiglas® V-811 acrylic resin, 1(b) was used. The samples were dried in 2
days in a hood at room temperature, 2 days in a vacuum oven at 85°C and finally for
1 hr. at 150°C.
2(d) Same as 2(a), except that in place of Plexiglas® V-811 acrylic resin, copolymer
1(d) was used.
2(e) Same as 2(a), except that in place of Plexiglas® V-811 acrylic resin, copolymer
1(e) was used.
2(f) Same as 2(a), except that in place of Plexiglas® V-811 acrylic resin, copolymer
1(f) was used.
B.2 DSC experiments.
[0042] Samples 2(a)1-6, 2(b)1-6, 2(d)1-6, 2(e)1-6 and 2(f)1-6 were all subjected to the
following DSC experiments using a heating rate of 20°C/min. and a quenching rate of
500°C/minute.
[0043] In the DSC experiment, each blend sample was subjected to multiple heating cycles.
The blend was first heated to just above the glass transition temperature, quenched,
and then annealed for 15 minutes at a selected temperature. The sample was then quenched
and heated once again to just above the glass transition temperature. After the final
heating, the sample was inspected for clarity. When the selected annealing temperature
was at or above the cloud point, the sample looked opaque. When the annealing temperature
was below the cloud point, the sample look transparent. In this way, a blend "phase
diagram" was estimated, and cloud point temperature was bracketed. In some case, the
observation of single or double Tg peaks in the thermograph was also used to determine
whether the sample had undergone phase separation. Since some of the copolymers have
Tg's very similar to that of PC, double peaks overlapped.
[0044] The results from the DSC experiments are shown in the plots of Figure 1. Temperatures
as a function of copolymer/PC composition is plotted. The temperature on the y-axis
corresponds to the annealing temperature of the experiment. An open circle indicates
that a transparent sample was observed after the heating cycle; a filled circle indicates
that an opaque sample was observed. For example, blend example 2(a) (80 wt% pMMA and
20 wt% PC) was opaque after annealing at 200°C. Another example is blend example 2(b)
(80 wt% copolymer 1(b) and 20 wt % PC), which was transparent after annealing at 240°C,
but opaque after annealing at 260°C. The cloud point for blend example 2(b) (80 wt%
copolymer 1(b) and 20 wt% PC) is therefore estimated to be between 240 and 260°C.
The DSC experiments clearly show that blending methyl methacrylate-tribromophenyl
maleimide copolymer with the polycarbonate raises the cloud point of the blend.

[0045] The plots in Figure 1 show how the apparent cloud point temperature increases with
increasing amount of TBPMI in the copolymer. All composition ratios of pMMA/PC (examples
2(a)1-6) had cloud points below 200°C. When 20 wt% TBPMI is incorporated into the
copolymer (examples 2(d)1-6), all composition ratios exhibited cloud points above
215°C. With 30 wt% TBPMI in the copolymer, (examples 2(e)1-6) all thecomposition ratios
exhibited cloud points above 220°C. Some of the composition ratios of examples 2(d)
and 2(e) remained clear even after annealing above 300°C.
[0046] As noted above, the observed cloud point behavior of samples prepared from solution
blends is not necessarily indicative of the thermodynamic phase behavior. Owing to
the difficulty of varying temperature during melt-blending, however, the DSC experiments
serve as a useful qualitative demonstration of the invention. The melt-blend experiments
described below quantitatively demonstrate that MMA/TBPMI copolymers form fully miscible
blends with PC at the desirable processing temperature.
B.3 Melt-blended examples
[0047] The following samples were melt-blended with a Haake Rheocord, at 250°C, for 3 mins.
at a mixing speed of 60 rpm.
3(a) The blends of this example consisted of pMMA (of example 1(a)) and PC (Makrolon®
2808 polycarbonate). Six composition ratios, by weight, were prepared: 1) 100 wt%
pMMA, 2) 80 wt% pMMA and 20 wt% PC, 3) 60 wt% pMMA and 40 wt% PC, 5) 20 wt% pMMA and
80 wt% PC, and 6) 100 wt% PC.
3(b) Same as 3(a), except copolymer 1(b) was used instead of pMMA.
3(c) Same as 3(a), except copolymer 1(c) was used instead of pMMA.
3(d) Same as 3(a), except copolymer 1(d) was used instead of pMMA.
3(e) Same as 3(a), except copolymer 1(e) was used instead of pMMA.
3(f) Same as 3(a), except copolymer 1(f) was used instead of pMMA.
[0048] The results of the melt-blend experiments are shown in Table 2. All composition ratios
of example 3(a), having 0 wt% TBPMI in the copolymer, were opaque when melt-blended
at 250°C. Some of the blend ratios of example 3(b), consisting of 10 wt% TBPMI in
copolymer, were transparent, depending on the amount of copolymer used in the blend,
and some were opaque, when melt-blended at 250°C. All of the blend ratios of examples
3(c), 3(d) and 3(e), having 15, 20 and 30 wt% TBPMI in copolymer, respectively, were
transparent when melt-blended with PC at 250°C. Therefore, by incorporating between
10 <wt% <30 TBPMI in the copolymer, it is possible to form single phase blends with
PC, at temperatures required for melt processing.

B.4 Comparative Example: TBPMI vs PMI
[0049] Applicants directly compared copolymers containing equimolar amounts of tribromophenyl
maleimide (TBPMI) and phenyl maleimide (PMI), in order to demonstrate the advantage
of TBPMI over PMI. Melt-processed blend examples 3(d) and 3(f) were compared; the
results are shown in Table 3. Whereas 6 mole% TBPMI in the copolymer results in transparent
blends at all blend ratios at 250°C, the non-brominated copolymer analog containing
6 mole% PMI results in opaque blends at all blend ratios.
Table 3 - TBPMI Copolymer vs PMI Copolymer -
Sample appearance. Column headings indicate example number and wt% Copolymer/PC in
blend. |
(C = Copolymer) |
|
|
|
|
Example |
Molar Amt. of maleimide in Copolymer |
80/20 wt% C/PC |
60/40 wt% C/PC |
40/60 wt% C/PC |
20/80 wt% C/PC |
3d |
6% TBPMI |
transparent |
transparent |
transparent |
transparent |
3f |
6% PMI |
opaque |
opaque |
opaque |
opaque |
[0050] DSC experiments were also conducted on examples 2(d) and 2(f). As shown in the plots
in Figure 2, all blend ratios of examples 2(f)1-6, with 6 mole% PMI in copolymer,
had apparent cloud points below 210°C. Blends with 6 mole% TBPMI incorporated into
the copolymer, examples 2(d)1-6, exhibit apparent cloud points above 215°C for all
blend ratios.
